Classifications

• • D—TEXTILES; PAPER
  • D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
  • D02G—CRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
  • D02G3/00—Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
  • D02G3/02—Yarns or threads characterised by the material or by the materials from which they are made
  • D02G3/04—Blended or other yarns or threads containing components made from different materials
• • D—TEXTILES; PAPER
  • D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
  • D02G—CRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
  • D02G3/00—Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
  • D02G3/44—Yarns or threads characterised by the purpose for which they are designed
  • D02G3/48—Tyre cords
• • D—TEXTILES; PAPER
  • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
  • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
  • D01D5/00—Formation of filaments, threads, or the like
  • D01D5/08—Melt spinning methods
  • D01D5/098—Melt spinning methods with simultaneous stretching
• • D—TEXTILES; PAPER
  • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
  • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
  • D01D5/00—Formation of filaments, threads, or the like
  • D01D5/12—Stretch-spinning methods
  • D01D5/16—Stretch-spinning methods using rollers, or like mechanical devices, e.g. snubbing pins
• • D—TEXTILES; PAPER
  • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
  • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
  • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
  • D01F6/78—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products
  • D01F6/80—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products from copolyamides
• • D—TEXTILES; PAPER
  • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
  • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
  • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
  • D01F6/78—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products
  • D01F6/80—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products from copolyamides
  • D01F6/805—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products from copolyamides from aromatic copolyamides
• • D—TEXTILES; PAPER
  • D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
  • D02G—CRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
  • D02G3/00—Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
  • D02G3/44—Yarns or threads characterised by the purpose for which they are designed
  • D02G3/446—Yarns or threads for use in automotive applications
• • D—TEXTILES; PAPER
  • D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
  • D02J—FINISHING OR DRESSING OF FILAMENTS, YARNS, THREADS, CORDS, ROPES OR THE LIKE
  • D02J1/00—Modifying the structure or properties resulting from a particular structure; Modifying, retaining, or restoring the physical form or cross-sectional shape, e.g. by use of dies or squeeze rollers
  • D02J1/22—Stretching or tensioning, shrinking or relaxing, e.g. by use of overfeed and underfeed apparatus, or preventing stretch
  • D02J1/222—Stretching in a gaseous atmosphere or in a fluid bed
• • D—TEXTILES; PAPER
  • D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
  • D02J—FINISHING OR DRESSING OF FILAMENTS, YARNS, THREADS, CORDS, ROPES OR THE LIKE
  • D02J1/00—Modifying the structure or properties resulting from a particular structure; Modifying, retaining, or restoring the physical form or cross-sectional shape, e.g. by use of dies or squeeze rollers
  • D02J1/22—Stretching or tensioning, shrinking or relaxing, e.g. by use of overfeed and underfeed apparatus, or preventing stretch
  • D02J1/224—Selection or control of the temperature during stretching
• • D—TEXTILES; PAPER
  • D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
  • D02J—FINISHING OR DRESSING OF FILAMENTS, YARNS, THREADS, CORDS, ROPES OR THE LIKE
  • D02J1/00—Modifying the structure or properties resulting from a particular structure; Modifying, retaining, or restoring the physical form or cross-sectional shape, e.g. by use of dies or squeeze rollers
  • D02J1/22—Stretching or tensioning, shrinking or relaxing, e.g. by use of overfeed and underfeed apparatus, or preventing stretch
  • D02J1/228—Stretching in two or more steps, with or without intermediate steps
• • D—TEXTILES; PAPER
  • D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
  • D02J—FINISHING OR DRESSING OF FILAMENTS, YARNS, THREADS, CORDS, ROPES OR THE LIKE
  • D02J1/00—Modifying the structure or properties resulting from a particular structure; Modifying, retaining, or restoring the physical form or cross-sectional shape, e.g. by use of dies or squeeze rollers
  • D02J1/22—Stretching or tensioning, shrinking or relaxing, e.g. by use of overfeed and underfeed apparatus, or preventing stretch
  • D02J1/229—Relaxing
• • D—TEXTILES; PAPER
  • D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
  • D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
  • D10B2331/00—Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products
  • D10B2331/02—Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products polyamides
• • D—TEXTILES; PAPER
  • D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
  • D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
  • D10B2505/00—Industrial
  • D10B2505/02—Reinforcing materials; Prepregs
  • D10B2505/022—Reinforcing materials; Prepregs for tyres
• • D—TEXTILES; PAPER
  • D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
  • D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
  • D10B2505/00—Industrial
  • D10B2505/12—Vehicles
  • D10B2505/124—Air bags

Definitions

• This invention relates to high strength polyamide yarns, as well as a process for preparing these yarns.
• High strength polyamide yarns are known and are for example applied in tyre cords, air bags.
• the yarns may be prepared from for example polyamide-6 or polyamide-66.
• tenacity values is a measure to define strength.
• Fiber tenacity can be measured, e.g. by a STATIMAT 4U automatic tensile testing machine, according to ASTM D885-04.
• STATIMAT 4U automatic tensile testing machine according to ASTM D885-04.
• EP2264235 discloses yarn for air bags comprising polyamide, in which the single fiber fineness is 1 to 2 dtex and in which strengths are reached of around 8.5 cN/dtex.
• a yarn comprising a copolyamide in an amount of at least 90 wt% with respect to the total weight of the yarn, which copolyamide comprises a) at least 95 wt% by weight with respect to the total weight of
• copolyamide monomeric units derived from hexamethylene diamine and adipic acid and
• the summed amount of monomeric units derived from X,Y and Z is between 0.1 to 4.5 wt% with respect to the total weight of the copolyamide and wherein the yarn has a tensile strength of at least 80 cN/tex as measured according to ASTM D885-04.
• Wt% is understood to be percentage by weight.
• molar ratio of monomeric units derived from X : monomeric units derived from Y is between 0.8 and 1.2, preferably between 0.9 and 1.1 and even more preferred between 0.95 and 1 .05.
• the monomeric units derived from X and Y are present in essentially equal molar amounts.
• a yarn according to the invention exhibits higher strengths as compared to a yarn which are made from a homopolyamide. Another advantage is that the yarns can be prepared by a simple process.
• homopolyamide herein is understood a polyamide which consists essentially of monomeric units derived from hexamethylene diamine and adipic acid. This polyamide is also referred to as PA-66.
• a copolyamide herein is understood to be a copolyamide which comprises besides a majority of monomeric units derived from hexamethylene diamine and adipic acid, further monomeric units derived from a diamine and a diacid and/or an aminoacid. These further monomeric units are thus different from hexamethylene diamine or adipic acid.
• Such copolyamide may be denoted as PA-66/XY, in which X refers to a further diamine and Y refers to a further diacid or PA-66/Z, in which Z refers to an aminoacid or PA-66/XY/Z.
• a copolyamide is to be distinguished from a blend, which is for example denoted as PA-66/PA-XY or PA-66/PA-Z.
• a blend is prepared by mixing two polyamides, whereas a copolyamide is prepared by mixing monomers which subsequently polymerize to a copolyamide.
• monomers is herein understood a molecule that when chemically bound to other monomers forms a polymer.
• potential monomers include for example aminoacids, diamines and diacids, as well as their salts.
• monomeric unit is herein understood a unit derived from a monomer as it is present in a polymer.
• Suitable cyclic monomeric units derived from diamines X include for example:
• C6 to C20 aromatic diamine such as m- or p-phenylenediamine
• C7 to C20 arylaliphatic diamine such as 4,4'-diaminodiphenylpropane, meta- xylylene diamine (MXD), para-xylylene diamine (PXD),
• C6 to C20 cyclic aliphatic diamine such as 1 ,4-diaminocyclohexane, 4- aminomethylcyclohexylamine, 5-Amino-1 ,3,3-trimethylcyclohexanemethylamine (also referred to as isophorone diamine, IPD), 3,3'-dimethyl-4,4'-diamino- dicyclohexylmethane, bis-(p-aminocyclohexane)methane, 2,2-di(4- aminocyclohexyl)-propane, 3,6-bis(aminomethyl)norbornane,
• the cyclic monomeric units derived from diamines X are monomeric units derived from C6 to C20 cyclic aliphatic diamines as listed above, as these exhibit a higher reactivity and are easier built in a copolyamide.
• Suitable cyclic monomeric units derived from dicarboxylic acids Y include for example:
• aromatic dicarboxylic acid such as naphthalene-2,6-dicarboxylic acid, naphthalene-1 ,4-dicarboxylic acid, isophthalic acid (I), terephthalic acid (T),
• arylaliphatic dicarboxylic acid such as o-, m- or p-phenylenediacetic acid, 4-methylisophthalic acid, 4-tert-butylisophthalic acid
• naphthalene dicarboxylic acids hydrogenated 2,6-naphthalene dicarboxylic acid, as well as 1 ,4-cyclohexane dicarboxylic acid, 1 ,3-cyclohexane dicarboxylic acid,
• the cyclic monomeric units derived from dicarboxylic acids are derived from isophthalic acid as this is easily dissolved in water and can be easier dosed.
• Another preferred cyclic monomeric unit is derived from terephthalic acid as this is readily available. Hydrogenated is herein understood that all aromatic rings are fully hydrogenated into a cyclic aliphatic unit.
• Suitable cyclic monomeric units derived from amino acids Z include monomeric units derived from 4-aminomethylcyclohexylcarboxylic acid, 4- aminocyclohexaneacetic acid, including cis and trans isomers thereof.
• the cyclic monomeric units derived from X and Y and/or Z have at least one cyclic structure containing 5 or 6 carbon atoms, such as a cyclo pentane structure, phenyl structure or cyclo hexane structure, which may for example be derived from 1 ,3 diaminocyclopentane, isophorone diamine, terephthalic acid, isophthalic acid.
• a cyclo pentane structure such as a cyclo pentane structure, phenyl structure or cyclo hexane structure, which may for example be derived from 1 ,3 diaminocyclopentane, isophorone diamine, terephthalic acid, isophthalic acid.
• the yarn comprises a copolyamide in an amount of at least 95 wt% with respect to the total weight of the yarn, which copolyamide comprises a) at least 95 wt% by weight with respect to the total weight of
• copolyamide monomeric units derived from hexamethylene diamine and adipic acid and
• the summed amount of monomeric units derived from X and Y is between 0.5 to 4.0 wt% with respect to the total weight of the copolyamide.
• monomeric units derived from X and Y are present in essentially equal molar amounts.
• a yarn comprising a copolyamide in an amount of at least 95 wt% with respect to the total weight of the yarn, which copolyamide comprises
• copolyamide monomeric units derived from hexamethylene diamine and adipic acid and
• diamine and cyclic monomeric units derived from a diacid Y chosen from isophthalic acid and terephthalic acid,
• the summed amount of monomeric units derived from X and Y is between 0.5 to 4.0 wt% with respect to the total weight of the copolyamide.
• the yarn comprises a copolyamide in an amount of at least 90 wt% with respect to the total weight of the yarn, preferably at least 95 wt% and most preferred at least 97 wt%.
• the yarn may comprise other additives which may be for example stabilizers as well as pigments.
• high tenacity, low titer, low hot air shrinkage (HAS) yarns are desired.
• the yarn according to the invention preferably has a titer of between 200 dtex and 700 dtex, more preferably between 300 dtex and 500 dtex and most preferred between 300 dtex and 400 dtex.
• a lower titer of the yarns allows weight savings, but also allows for example more compact, better foldable fabrics prepared from the yarn, such as for example in applications of air bags.
• low titer yarns are preferably used in combination with a high tenacity.
• the usage of 450 dtex to 500 dtex yarns typically requires a yarn with a tenacity of at least 80 cN/tex.
• the yarn according to the invention exhibits a tensile strength of at least 80 cN/tex as measured according to ASTM D885-04, preferably the yarn has a tensile strength of at least 85 cN/tex and more preferably at least 90 cN/tex.
• Yarns with a tensile strength of at least 80 cN/tex are also herein referred to as technical yarns, in contrast to textile yarns.
• Textile yarns usually have lower tensile strength and are usually not suitable for applications in which technical yarns are employed.
• the yarn has a titer of between 300 dtex and 400 dtex and a tenacity of at least 85 cN/tex, most preferred the yarn has a titer of between 300 dtex and 400 dtex and a tenacity of at least 90 cN/tex, as this allows thinner fabrics with higher strength.
• the yarn according to the invention has a hot air shrinkage of at most 8.0%, preferably at most 5.0%, as this allows for higher dimensional stability.
• HAS is measured at 177 °C after 2 min, as explained below.
• Minimum HAS values may be as low as 1 .0%.
• the yarn according to the invention has a
• HAS HAS of at most 8.0 %, preferably at most 5.0% and a tenacity of at least 80 cN/tex, preferably at least 85 cN/tex, and a titer of between 200 dtex and 700 dtex, preferably between 300 dtex and 500 dtex.
• bobbins containing the yarns were conditioned for at least 12 hours in a 55% relative humidity 23°C atmosphere.
• Tensile strength of fibers also known as tenacity, is measured according to ASTM D885-04 and given in cN/dtex or cN/tex. The measurement was performed using STATIMAT 4U automatic tensile testing machine.
• Fiber titer also referred to as linear density, measured in dtex, is defined as weight in grams of 10000 meters of yarn. The titer can be measured by weighing a piece of yarn of a known length, usually 20 meters, on a balance with accuracy of 0.001 g and then recalculating the weight of 10000 meters of yarn. In practice, the titer measurement is automated and performed by STATIMAT 4U as well.
• Hot air shrinkage is measured according to ASTM D4974-04 at 177°C for 2 minutes using Testrite shrinkage measurement instrument under a load of 5 mN/tex.
• a process for preparing a yarn according to the present invention generally comprises the following steps and is further referred to as process A:
• composition comprising a copolyamide to an extruder and melting it, optionally mixing with additives, such as stabilizer or pigment, to obtain a molten composition;
• the molten composition is extruded through a spinneret to form filaments, which are subsequently stretched, cooled and combined to form at least one yarn;
• the at least one yarn is subsequently subjected to a drawing process at a temperature of between 25 °C and 265 °C to a draw ratio of between 4 and 6.
• the drawing is carried out at a temperature between 50 °C and 215 °C.
• the drawing may be performed, e.g., by means of pairs of heated draw rolls, heated hot air ovens, etc;
• the yarn is subjected to a relaxation and/or a heat set step
• the at least one yarn is wound up.
• the at least one yarn is wound up on a bobbin.
• the composition is molten and, if necessary, mixed with additives such as for example stabilizers, pigments, in an extruder (01 ) and further extruded through a spinneret (03) to form filaments.
• the filaments (05) are cooled, drawn and combined to at least one yarn between the spinneret (03) and take up rolls (07).
• the yarn is heated up by a pair of rolls (1 1 ) to a temperature between 50°C and 80°C and drawn 2 to 3 times in air gap (12) between pairs of rolls (1 1 ) and (21 ). Then, the yarn is heated up by a pair of rolls (21 ) to a temperature between 120°C and 245 °C and drawn 1.35 to 3 times in air gap (22), between pairs of rolls (21 ) and (31 ), resulting in a draw ratio between 4 and 6.
• the drawing steps are followed by heat setting and relaxation: the yarn is heated up to the temperatures of 200 °C to 245 °C by a pair of rolls (31 ) and relaxed by 0% to 10% in the air gap (32) between the pairs of rolls (31 ) and (41 ). Finally, the yarn is wound up on a bobbin by a reel device (91 ).
• the yarn according to the invention is preferably made by a process, hereafter referred to as process B, which comprises the following steps: Providing a composition comprising a copolyamide to an extruder and melting it, optionally mixing with additives, such as stabilizer or pigment, to obtain a molten composition;
• the molten composition is extruded through a spinneret to form filaments, which are subsequently stretched, cooled and combined to form at least one yarn;
• the at least one yarn is subsequently subjected to a drawing process at a temperature between 25 °C and 265 °C to a draw ratio of between 4 and 6.
• a drawing process at a temperature between 25 °C and 265 °C to a draw ratio of between 4 and 6.
• the drawing is carried out at a temperature between 50 °C and 215 °C.
• the drawing may be performed, e.g., by means of pairs of heated draw rolls, heated hot air ovens, etc.
• the yarn After drawing, the yarn is relaxed by from 4% to 10% in at least three stages while being kept in a temperature range of 250 °C to 260 °C.
• the at least one yarn is wound up.
• the at least one yarn is wound up on a bobbin.
• the temperature during relaxation is higher than the highest temperature during drawing. This has the advantage that the relaxation is more effective. More preferably, the temperature during relaxation is increased in each subsequent stage. This has the advantage that sufficient yarn tension is maintained between the relaxation rolls, which avoids breaking of the yarn.
• process B yields yarns with a lower hot air shrinkage as compared to process A.
• FIG. 2 An example of the apparatus to perform process B is illustrated in Figure 2.
• the difference between Figure 2 and the process described in Figure 1 is that five heated roll pairs (1 1 ), (21 ), (31 ), (41 ), (51 ) are employed, instead of four.
• the extrusion (01 ), the spinneret (03), the air gap (05), the take up rolls (07) as well as the first two roll pairs (1 1 ), (21 ) conditions can be chosen in the same way as in the process A, as illustrated in Figure 1.
• rolls (31 ) ,(41 ) and (51 ) have to be set to a temperature of between 250 °C and 260°C, the yarn being relaxed by from 4% to 10% in the at least three stages (32), (42), (52).
• the yarn is subsequently wound up on a reel device (91 ).
• a 350dtex yarn consisting of 72 filaments is prepared from a copolyamide PA66/IPDT according to process A.
• the copolyamide is synthesized from a mixture of hexamethylene diamine, adipic acid, isophorondiamine (IPD), and terephthalic acid (T).
• the monomeric unit derived from IPD was 0.5 wt% with respect to the copolyamide and the monomeric unit derived from T was 0.5 wt% with respect to the copolyamide.
• the remainder of the copolyamide are monomeric units derived from hexamethylene diamine and adipic acid, thus 99 wt%.
• the process is applied using an apparatus as illustrated in Figure 1 .
• the yarn is drawn in a two-step process to a draw ratio of 5.0.
• relaxation of in total 6% is applied between the 3 rd and the 4 th rolls pair and between the 4 th rolls pair and the reeling device.
• the yarn has an expected tenacity of about 93 cN/tex, elongation at break of 20%, and an expected hot air shrinkage, at 177°C 2min, of about 7 %.
• the same copolyamide is used as in the Example 1.
• the yarn is prepared according to process B using an apparatus as illustrated in Figure 2. After take up, the yarn was drawn in a two-step process to a draw ratio of 4.9. After hot drawing, three-step relaxation process of in total 10% has been applied between the 3 rd and the 4 th rolls pair, between the 4 rd and the 5 th rolls pair and between the 5 th rolls pair and the reeling device.
• the yarn has an expected tenacity of 90cN/tex, elongation at break of 22%, titer of 350 dtex, and an expected hot air shrinkage, at 177°C 2min, of 4%.
• a 350dtex yarn consisting of 72 filaments is prepared from a homopolyamide PA66 according to process A.
• the homopolymer is synthesized from hexamethylene diamine and adipic acid contributing 100wt% of the monomers.
• the yarn After hot drawing, relaxation of in total 6% is applied between the 3 rd and the 4 th rolls pair and between the 4 th rolls pair and the reeling device.
• the yarn has an expected tenacity of 85cN/tex, elongation at break of 18%, and an expected hot air shrinkage, at 177°C 2min, of 6%.
• Example A and the yarn is prepared according to process B using an apparatus as illustrated in Figure 2. After take up, the yarn is drawn in a two-step process to a draw ratio of 4.3.
• the yarn has an expected tenacity of 81 cN/tex, elongation at break of 25%, titer of 350 dtex, and expected hot air shrinkage, at 177°C 2min, of 4 %.
• the examples show the advantages of the yarn according to the invention as compared to a yarn prepared from a homopolyamide.
• Example 1 shows, the yarn according to the invention can be drawn to a draw ratio of 5.0 and reaches a tenacity of about 93cN/tex.
• Comparative example A shows, a homopolyamide being spun at very similar conditions can be drawn only 4.5 times resulting in a yarn with tenacity of about 85cN/tex, which is approximately 10% lower than the yarn made with the copolyamide from the Example 1 .
• Example 2 illustrates that if a process B is employed yarns with a tenacity of about 90cN/tex and low hot air shrinkage can be obtained by employing the copolyamide.

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• Engineering & Computer Science (AREA)
• Textile Engineering (AREA)
• Mechanical Engineering (AREA)
• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• General Chemical & Material Sciences (AREA)
• Artificial Filaments (AREA)
• Polyamides (AREA)
• Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
• Air Bags (AREA)

Applications Claiming Priority (2)

Publications (1)

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Family Applications (1)

Country Status (6)

Families Citing this family (1)

Family Cites Families (24)

• 2016
  • 2016-02-23 US US15/551,633 patent/US10370780B2/en not_active Expired - Fee Related
  • 2016-02-23 WO PCT/EP2016/053734 patent/WO2016135122A1/en active Application Filing
  • 2016-02-23 JP JP2017543374A patent/JP2018508664A/ja active Pending
  • 2016-02-23 EP EP16707018.4A patent/EP3262218A1/en not_active Withdrawn
  • 2016-02-23 KR KR1020177026604A patent/KR20170120652A/ko unknown
  • 2016-02-23 CN CN201680011347.3A patent/CN107429440A/zh active Pending
• 2019
  • 2019-06-19 US US16/446,489 patent/US20190301057A1/en not_active Abandoned

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